Hydrotreating with silicon removal
    31.
    发明授权
    Hydrotreating with silicon removal 失效
    加氢处理除硅

    公开(公告)号:US5118406A

    公开(公告)日:1992-06-02

    申请号:US693369

    申请日:1991-04-30

    IPC分类号: C10G45/08

    CPC分类号: C10G45/08

    摘要: A catalytic hydrotreating process wherein silicon-containing contaminants contained in a hydrocarbon feedstream are deposited onto a hydrotreating catalyst bed during hydrotreating in a manner providing improved catalyst stability. Hydrotreating catalysts having relatively high activities and low surface areas are located downstream of upstream hydrotreating catalysts having relatively low activities and high surface areas.

    摘要翻译: 催化加氢处理方法,其中包含在烃进料流中的含硅污染物以提供改进的催化剂稳定性的方式在加氢处理期间沉积在加氢处理催化剂床上。 具有较高活性和低表面积的加氢处理催化剂位于具有较低活性和高表面积的上游加氢处理催化剂的下游。

    Method for multi-staged hydroprocessing
    32.
    发明授权
    Method for multi-staged hydroprocessing 有权
    多级加氢处理方法

    公开(公告)号:US08518241B2

    公开(公告)日:2013-08-27

    申请号:US12495574

    申请日:2009-06-30

    IPC分类号: C10G65/12 C10G69/02

    CPC分类号: C10G65/02 C10G65/10

    摘要: Methods for processing a hydrocarbonaceous feedstock flows are provided. In one aspect, the method includes providing two or more hydroprocessing stages disposed in sequence, each hydroprocessing stage having a hydroprocessing reaction zone with a hydrogen requirement and each stage in fluid communication with the preceding stage. A hydrogen source is provided substantially free of hydrogen from a hydrogen recycle compressor. The hydrocarbonaceous feedstock flow is separated into an portions of fresh feed for each hydroprocessing stage, and the first portion of fresh feed to the first hydroprocessing stage is heated. The heated first portion of fresh feed is supplied with hydrogen from the hydrogen source in an amount satisfying substantially all of the hydrogen requirements of the hydroprocessing stages to a first hydroprocessing zone. The unheated second portion of fresh feed is admixed with effluent from previous stage to quench the hot reactor effluent before entering a second stage.

    摘要翻译: 提供了处理含烃原料流的方法。 一方面,该方法包括提供依次设置的两个或多个加氢处理阶段,每个加氢处理阶段具有氢需求的加氢处理反应区,每个阶段与前一阶段流体连通。 从氢循环压缩机中提供基本上不含氢气的氢源。 将烃原料流分离成每个加氢处理阶段的新鲜进料部分,并且加热到第一加氢处理阶段的新鲜进料的第一部分。 新鲜进料的加热的第一部分从氢源供应氢气,其数量满足加氢处理阶段的大部分氢气需求量至第一加氢处理区域。 将新鲜饲料的未加热的第二部分与前一阶段的流出物混合以在进入第二阶段之前骤冷热反应器流出物。

    Liquid phase hydroprocessing with temperature management
    33.
    发明授权
    Liquid phase hydroprocessing with temperature management 有权
    液相加氢处理与温度管理

    公开(公告)号:US08314276B2

    公开(公告)日:2012-11-20

    申请号:US13187006

    申请日:2011-07-20

    摘要: A method of hydroprocessing hydrocarbons is provided using a substantially liquid-phase reactor having first and second catalyst beds with a heat transfer section positioned therebetween. The first and second catalyst beds and the heat transfer section are combined within the same reactor vessel. Each catalyst bed having an inlet temperature and an exit temperature and having a hydroprocessing catalyst therein with a maximum operating temperature range. The method hydroprocesses the hydrocarbons and removes sufficient heat from the hydrocarbons using the heat transfer section so that the exit temperature of the hydrocarbons existing the first catalyst bed is substantially maintained below the maximum operating temperature range of the hydroprocessing catalysts in the first bed and, at the same time, also providing the hydrocarbons to the second catalyst bed at the inlet temperature so that the exit temperature of the hydrocarbons at the exit of the second catalyst bed also does not exceed the maximum operating temperature range of the hydroprocessing catalyst in the second bed.

    摘要翻译: 使用基本上液相反应器提供加氢处理烃的方法,该反应器具有位于其间的传热部分的第一和第二催化剂床。 第一和第二催化剂床和传热部分在同一反应器容器内组合。 每个催化剂床具有入口温度和出口温度,并且其中具有最大工作温度范围的加氢处理催化剂。 该方法加氢处理烃并使用传热部分从烃中除去足够的热量,使得存在第一催化剂床的烃的出口温度基本上保持在第一床中的加氢处理催化剂的最大工作温度范围内,并且在 同时,还在入口温度下将烃提供给第二催化剂床,使得第二催化剂床出口处的烃的出口温度也不超过第二床中的加氢处理催化剂的最大工作温度范围 。

    Hydrotreating Processes for Fabricating Petroleum Distillates from Light Fischer-Tropsch Liquids
    34.
    发明申请
    Hydrotreating Processes for Fabricating Petroleum Distillates from Light Fischer-Tropsch Liquids 审中-公开
    从轻的费 - 托液制造石油馏分的加氢处理方法

    公开(公告)号:US20120269695A1

    公开(公告)日:2012-10-25

    申请号:US13534586

    申请日:2012-06-27

    申请人: Peter Kokayeff

    发明人: Peter Kokayeff

    IPC分类号: B01J8/00 B01J19/00 B01J10/00

    摘要: A method for obtaining a petroleum distillate product is provided, the method includes subjecting an untreated light Fischer-Tropsch liquid to a two-step hydrogenation process, each step to be carried in the presence of a catalyst comprising an amorphous substrate having a metallic composition embedded therein. After the first step of hydrogenation, an intermediate hydrotreated light Fischer-Tropsch liquid is obtained, followed by the second step of hydrogenation thereof, obtaining the petroleum distillate product as a result. An apparatus for carrying out the method is also provided.

    摘要翻译: 提供了一种获得石油馏出物产品的方法,该方法包括使未经处理的费 - 托液体进行两步氢化处理,每个步骤在催化剂存在下进行,该催化剂包含嵌入金属组成的非晶基材 其中。 在氢化的第一步骤之后,获得中间体加氢处理的费 - 托液,随后进行第二步氢化,得到石油馏分产物。 还提供了一种用于执行该方法的装置。

    METHODS FOR PRODUCING DIESEL RANGE MATERIALS HAVING IMPROVED COLD FLOW PROPERTIES
    35.
    发明申请
    METHODS FOR PRODUCING DIESEL RANGE MATERIALS HAVING IMPROVED COLD FLOW PROPERTIES 审中-公开
    用于生产具有改进的冷流特性的柴油机系列材料的方法

    公开(公告)号:US20120090223A1

    公开(公告)日:2012-04-19

    申请号:US12903874

    申请日:2010-10-13

    摘要: Embodiments of a method for producing a diesel range material having improved cold flow properties are provided. In one embodiment, the method includes the steps of providing a waxy diesel range feedstock, producing an intermediary product stream containing a predetermined amount of oxygenated organocompounds from the waxy diesel range feedstock, and contacting the intermediary product stream with a dewaxing catalyst under process conditions at which the oxygenated organocompounds chemically interact with the dewaxing catalyst to convert a portion of the n-paraffins within the intermediary product stream to iso-paraffins while minimizing cracking of the diesel range material.

    摘要翻译: 提供了具有改善的冷流特性的柴油范围材料的制造方法的实施例。 在一个实施方案中,该方法包括以下步骤:提供蜡质柴油范围原料,产生含有来自蜡质柴油范围原料的预定量的含氧有机化合物的中间产物流,并在中间产物流与脱蜡催化剂在工艺条件下接触 其中氧化的有机化合物与脱蜡催化剂化学相互作用以将中间产物流中的一部分正链烷烃转化为异链烷烃,同时使柴油范围材料的破裂最小化。

    Hydrocarbon conversion process to improve cetane number
    39.
    发明授权
    Hydrocarbon conversion process to improve cetane number 有权
    烃转化过程提高十六烷值

    公开(公告)号:US07790020B2

    公开(公告)日:2010-09-07

    申请号:US11872102

    申请日:2007-10-15

    IPC分类号: C10G45/44 C10G65/02

    CPC分类号: C10G45/02 C10G2400/04

    摘要: A process is provided for producing low sulfur diesel having a high cetane number where the temperature and pressure requirements for obtaining low levels of sulfur is separated from the temperature and pressure requirements for improving cetane. In one aspect, a low pressure hydrodesulfurization zone and a high pressure aromatic saturation zone are employed to sequentially achieve the desired sulfur and cetane levels. In another aspect, the process first converts a diesel boiling range hydrocarbonaceous stream in a hydrotreating zone at conditions effective to produce a hydrotreating zone effluent having a reduced concentration of sulfur with minimal saturation of aromatics. Hydrogen is then admixed with the hydrotreating zone effluent, which is then reacted in a substantially liquid-phase continuous reaction zone substantially undiluted with other streams to effect saturation of aromatics to provide a liquid-phase continuous reaction zone effluent having an improved cetane number.

    摘要翻译: 提供了一种生产具有高十六烷值的低硫柴油的方法,其中获得低水平硫的温度和压力要求与用于改善十六烷的温度和压力要求分离。 一方面,使用低压加氢脱硫区和高压芳族饱和区来顺序地获得所需的硫和十六烷值。 在另一方面,该方法首先在加氢处理区中转化柴油沸程烃流,其条件是有效地产生具有降低的硫浓度并且具有最小芳烃饱和度的加氢处理区流出物。 然后将氢气与加氢处理区流出物混合,然后将其在基本上液相连续的反应区中与基本上未稀释的其它流反应,以实现芳族化合物的饱和,以提供具有改进的十六烷值的液相连续反应区流出物。

    Hydrodesulfurization process
    40.
    发明授权
    Hydrodesulfurization process 失效
    加氢脱硫工艺

    公开(公告)号:US07749375B2

    公开(公告)日:2010-07-06

    申请号:US11852174

    申请日:2007-09-07

    IPC分类号: C10G45/04 C10G45/08

    摘要: In one aspect, a hydrodesulfurization process is provided that selectively desulfurizes a hydrocarbon stream with minimal olefin saturation and minimal recombination of sulfur into mercaptans. In another aspect, the process includes a multi-stage reaction zone including at least first and second serial hydrodesulfurization reaction zones that sequentially remove sulfur from a hydrocarbon stream. In yet another aspect, the process is particularly suited to selectively desulfurize an olefinic naphtha hydrocarbon stream, such as FCC naphtha, steam cracked naphtha, coker naphtha, or other gasoline boiling hydrocarbon streams.

    摘要翻译: 在一个方面,提供加氢脱硫方法,其选择性地使烃流以最少的烯烃饱和度和硫的最小重组硫化为硫醇。 在另一方面,该方法包括多级反应区,其包括至少第一和第二连续加氢脱硫反应区,其顺序地从烃流中除去硫。 在另一方面,该方法特别适用于烯烃石脑油烃流选择性脱硫,例如FCC石脑油,蒸汽裂解石脑油,焦化石脑油或其他汽油沸腾烃流。